US3816344A - Process for producing a catalyst - Google Patents

Process for producing a catalyst Download PDF

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US3816344A
US3816344A US00265449A US26544972A US3816344A US 3816344 A US3816344 A US 3816344A US 00265449 A US00265449 A US 00265449A US 26544972 A US26544972 A US 26544972A US 3816344 A US3816344 A US 3816344A
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carrier
solution
noble metal
producing
chloride
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S Shimizu
T Iwase
H Hara
R Hori
S Sakurai
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Toyota Motor Corp
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Toyota Motor Corp
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/44—Palladium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/944—Simultaneously removing carbon monoxide, hydrocarbons or carbon making use of oxidation catalysts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/42—Platinum
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56—Platinum group metals
    • B01J23/64—Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/652—Chromium, molybdenum or tungsten
    • B01J23/6522—Chromium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0201—Impregnation
    • B01J37/0205—Impregnation in several steps
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/16—Reducing

Definitions

  • ABSTRACT A film of a noble metal is deposited on the surface of a carrier without substantial penetration of the carrier by immersing the carrier first in a dilute solution of a salt of the noble metal, removing the carrier and heating and drying it to produce precipitation cores of the noble metal on the surface of the carrier, and then immersing the carrier with the precipitation cores in a solution of a noble metal salt which also contains a reducing agent for the salt and a stabilizer for the solution.
  • the film of noble metal thus produced on the surface is adherent thereto and is highly active as a catalyzer for removing pollutants from the exhaust gas of an automobile.
  • This invention relates to a process for producing a catalyst or catalyzer to be used for various chemical renoble metal may be as much as ten or more times as effective as the base metal.
  • Catalysts which may be used for these reactions include base metals such as copper, chromium, nickel, manganese, vanadium, cobalt or one of the noble metals such as, for example, platinum, palladium and rhodium.
  • the conventional method for producing this type of carrier-catalyzer is to impregnate the carrier with a solution which contains the catalytic metal.
  • the metal may be activated by any appropriate means such as by heating or with a reducing agent.
  • the catalytic activity is due primarily to the catalyst deposited on the carrier surface, but the catalyzer metal applied by impregnation penetrates the carrier so deeply that its efficiency drops to as low as l0l percent. In other words, only a small percentage of the metal can contribute to catalysis.
  • the impregnation process takes a long time. Usually, from 5 to 6 hours are required, but depending on the type of carrier and the purpose, twenty or more hours may be required.
  • a new method for making a catalyst has been disclosed in Japanese Pat. Publication Sho 46-22442.
  • a catalyst carrying a base metal such as copper, nickel, chromium, or zinc is produced by a chemical plating process.
  • a series of steps, including sensitization, activation and nonelectrolytic precipitation are required.
  • the reaction involves reducing palladium chloride with stannous chloride and precipitating palladium on a core metal.
  • base metals are not as effective as the noble metals as a catalyst.
  • the catalysts of Table l were carried on 'y-alumina grains. Each carrier contained 0.2 weight percent noble metal and 10 weight percent base metal.
  • Test conditions for measurement were as follows: Gas composition C H (57O ppm )+CO( 1.2 percent)+0 (2 percent) +N (balance) Flow rate 1.5 l/min.
  • Catalyzer bed temperature 350 C Space velocity 18,000 hr.
  • the noble metals are highly effective elements as a purifying catalyzer for exhaust gases, but they are so expensive that it is extremely important to make effective use of them with high material efficiency.
  • the present invention has been perfected by the inventors through persistent efforts to eliminate the drawbacks to the conventional method.
  • Another object of the invention is to provide a method for depositing a noble metal on a carrier to produce a catalyst of improved effectiveness for use in removing harmful gases from the exhaust gas of an automobile.
  • a further object of the invention is to provide a method for depositing a noble metal as a film over a carrier surface without substantial penetration of the carrier by the metal.
  • a more specific object of the invention is to provide a simple but effective method for depositing a catalytic metal on the surface of a carrier therefor.
  • the metal is so disposed on the surface of the carrier that it is available for catalysis of chemical reactions which remove poisonous gases such as hydrocarbons, carbon monoxide and nitrogen oxides from exhaust gas of an automobile.
  • the noble metal since the noble metal is confined primarily to the surface of the carrier, substantially all of it is available for contact by the exhaust gases as they flow rapidly over the carrier in the exhaust system of an automobile.
  • the noble metal catalyst is carried only on the carrier surface, the amount of metal required is less than that required by the impregnation method, yet the catalysis obtained is more than equivalent to that of the impregnated carrier and the material efficiency is extremely high.
  • the catalyst provided by this invention is particularly advantageous for purification of automobile exhaust gas because such gas travels at such a high velocity chemical reaction is limited to the vicinity of the external surface of the carrier.
  • the adhesion of metal to the carrier is much greater than that of metal deposited on a carrier by impregnation because the reducing reac tion forms a noble metal film directly on the rough surface of the carrier.
  • the conventional method takes a fairly long time for impregnation, but according to the present invention the catalytic noble metal film can be formed in a few minutes. Moreover, the catalytic film needs no post treatment except drying and can be used immediately without reduction or heat treatment to activate the catalyst. Thus in terms of net manufacturing time, the method provided by this invention is /3 to A as long as the conventional impregnation method.
  • the process provided by the invention can be divided into the steps of carrier pretreatment, precipitation core seeding and catalyzer-film formation.
  • the carrier pretreatment serves two purposes. One purpose is cleaning of the carrier and this may be done in the same manner as the conventional pretreatment ofa common metal surface. The other purpose is to counteract any catalyst poison which may have infiltered the carrier during its manufacture. This can be done by neutralization and heating. After the pretreatment, ample washing and drying is needed to remove all of the treating solution. This pretreatment, however, may be skipped in some instances depending upon the carrier manufacturing method, the carrier surface condition and the type and use of the carrier.
  • a solution containing a noble metal salt, a stabilizer and a reducing agent which has been adjusted to an adequate range of concentrations is brought into contact with the carrier by immersion or other method to form a catalytic noble metal film on the surface of the carrier.
  • the carrier and film are then heated and dried to provide a catalyst ready for use in the exhaust system of an automobile.
  • any suitable carrier may be used for the present invention.
  • alumina, silica, magnesia or mixtures thereof, such as ceramics are used.
  • a metal may also be employed as the carrier.
  • harmful substances such as sulfur radicals or phosphorus which may poison the catalyst should be neutralized with, say, 28 percent ammonia water. Any undesirable organic matter should be removed by heating the carrier to 500600 C.
  • some carriers may need pretreatment; in this pretreatment, however, use of a chemical which is likely to produce a catalyst poison like sulfuric acid should be avoided.
  • a dilute solution of a noble metal is used for precipitation-core seeding the carrier surface to promote the precipitation by chemical reduction and uniform growth of noble metal film during the film forming step.
  • aqueous solutions of a nitrate or a hydrochloride of gold, platinum, rhodium or palladium at a concentration of from 0.0005 to ().l mol per liter.
  • the concentration should be limited to 0. l mol per liter, because at a higher concentration than this, the noble metal will diffuse in the solution in the next step before precipitation with the result that aging of the solution is promoted and a loss of expensive noble metal occurs.
  • the solution for precipitation seeding may be employed as neutral aqueous solution, but in order to obtain a high concentration of a salt of low water solubility, it is better to add nitric acid or hydrochloric acid at a rate of 5 to milliliters per liter of solution.
  • the nitric acid and hydrochloric acid concentration suggested is based on theme of 60 percent nitric acid or 35 percent hydrochloric acid for addition to the noble metal salt solution.
  • the temperature may be room temperature. Heating to 5060 C will accelerate subsequent precipitation of the catalytic metal, but if the temperature is too high, aging will be promoted. Thus the most desirable range of temperatures is l5-25 C. Use of an alkaline complex salt instead of a nitrate or a hydrochloride is also possible.
  • stannous chloride is employed for palladium seeding to precipitate a metal on the non-conductive surface.
  • the catalytic noble metal is obtained by simply immersing the carrier in a thin solution of a noble metal. This avoids poisoning of the catalyst by stannous chloride.
  • the working principle of the catalytic noble metal film being formed is as follows:
  • the noble metal salt solution is stabilized by a stabilizing agent mainly composed of a complexing agent and a chelating agent and a reducing precipitation is caused by some appropriate reducing agent to grow around the cores previously seeded on the carrier surface.
  • a stabilizing agent mainly composed of a complexing agent and a chelating agent
  • a reducing precipitation is caused by some appropriate reducing agent to grow around the cores previously seeded on the carrier surface.
  • the three components i.e., noble metal salt, stabilizing agent and reducing agent are to be described.
  • Suitable metal salts include chloroplatinic acid, platinum chloride, palladium chloride, palladium nitrate, palladium sulfate, palladium tetraamine, rhodium chloride, rhodium sulfate, rhodium nitrate and the like.
  • the quantity of noble metal salt used in the solution will vary some depending upon the particular salt used, but it will usually be within the range of 0.005 to 0.1 mol per liter of solution. The preferred amount is from about 0.01 to 0.05 mol noble metal salt per liter ofsolution. Particularly when a precipitation with a wide surface area is required, the ratio of reducing agent to noble metal salt must be reduced.
  • the stabilizing agent is adopted to prevent natural decomposition of the solution.
  • the noble metal salt may be reduced to the metal by the reducing agent if no stabilizing agent is present in the solution. ln other cases, a too rapid decomposition of the solution may occur during film formation and shorten the life of the solution.
  • the stabilizing agent is added to the solution so that the solution will remain stable without change, except by deposition of metal on the carrier while it is immersed therein.
  • the solution is decomposed as the result of the reducing agent in the solution combining with metal ions or of the metal ions settling due to the pH change, etc. To prevent this, the pH change is inhibited by adding a weak acid with a certain dissociation constant, for example, an organic acid or its alkaline salt.
  • additives can work not only as a pH buffer, but also as a complexing agent for metal ions. Free metal ions in excess of the reducing agent may be complexed by the complexing agent to avoid decomposition. But if the complexing agent used is one that produces too stable a complex substance, the concentration of the free metal-ions becomes too low and the rate of precipitation is retarded. Thus, in the selection of a complexing agent, the reactivity of a complex substance obtained as well as its dissociation constant must be taken into account.
  • the stabilizing agents available include the disodium salt of ethylenediamine tetraacetic acid and Rochelle salt, which form a complex compound of a noble metal; and hydroxycarboxylic acids that form a stable metal chelate, namely, glycollic acid, malic acid, lactic acid, tartaric acid, citric acid and the like.
  • hydroxycarboxylic acids that form a stable metal chelate, namely, glycollic acid, malic acid, lactic acid, tartaric acid, citric acid and the like.
  • an acid with many carboxylic radicals in the molecule such as citric acid.
  • the sodium salt of polycarboxylic acids may be used for higher solubility.
  • Other suitable stabilizing agents include inorganic ammonium salts of a basic nature such as ammonium chloride, ammonium nitrate and ammonium sulfate.
  • fatty ketones and fatty sulfites are also effective; for instance, methyl ethyl keton, acetone and 2,2- dithioethanol.
  • the necessary quantity of stabilizer differs depending upon the substance employed, but commonly, it is in the range of 0001-05 mol per liter of solution or preferably 0.0050.0l mol per liter.
  • Suitable reducing agents include formalin, sodium formate, sodium hypophosphite, hydrazine, hydrosulfite, hydroboric acid, sodium borohydride hydroquinone, urea and the like. There is considerable variation in the reducing ability of such compounds.
  • the noble metal may fail to precipitate at all or, on the contrary, may precipitate too fast to deposite on the carrier and as a result, it may be dispersed in a colloidal form in the solution.
  • the required quantity of reducing agent is 0.050.5 mol per liter and for the best results, it should be 0.1-0.2 mol per liter. When great quantities of reducing agent are to be used, they must be added at a rate matching the rate of reaction.
  • 'y-alumina grains are used as the carrier. They are carefully washed with distilled water; dried and then fired at 600C for two hours in an electric furnace. After being left to cool, they are immersed for about 20 minutes at room temperature in a solution of palladium chloride having a concentration of about 1 gram per liter and containing about milliliters hydrochloric acid per liter. Then they are dried in hot air and again in the electric furnace for 30 minutes at 140 C.
  • the resulting seeded carrier which provides cores for precipitation, is immersed in a solution which has been prepared by dissolving 2 grams of palladium chloride in about 300 ml of 28 percent ammonia water to form a solution of an ammonium complex salt tetramine palladium, adding thereto a stabilizer, i.e., 5g of the disodium salt of ethylenediamine tetra acetic acid, then adding pure water to make one liter of solution. Just prior to use, several drops of hydrated hydrazine are added to the solution as a reducing agent. The solution at room temperature reacts with a vigorous generation of hydrogen gas upon immersion of the seeded carrier and in a few minutes palladium is reductionprecipitated on the carrier surface, thus producing the desired catalyzer.
  • a stabilizer i.e., 5g of the disodium salt of ethylenediamine tetra acetic acid
  • y-alumina grains are used as the carrier. They are completely washed with distilled water; dried and then fired in an electric furnace at 600 C for 2 hours. After being left to cool, the carrier is immersed for about 20 minutes at room temperature in a solution of 10 grams chloroplatinic acid per liter. Then it is exposed to hot air and again dried in an electric furnace for 30 minutes at 140 C, thereby seeding the carrier surface with cores of noble metal for precipitation. A solution of 2g chloroplatinic acid and lg disodium salt of ethylenediamine tetra acetic acid in about 500 ml of water is prepared. A solution of 4g sodium formate and 9g sodium carbonate anhydride in about 100 ml of water is also prepared.
  • chromium fluoride About 200 ml of water are heated to about 60 C and 17g of chromium fluoride are dissolved therein. After complete dissolution, about 200 ml of water are added and an additional 1g of chromium chloride and 9g of sodium citrate are dissolved therein to make a total volume of 1 liter. Then, using a one normal solution of caustic soda, this solution is adjusted to a pH of 9:0.5, heated to about C and mixed with 9g of sodium hypophosphite to make a processing solution. In the same way as in Example 1, a preliminarily seeded carrier is immersed in this processing solution for about 10 minutes and a gray chromium film is formed on the carrier surface.
  • the catalyzer thus obtained is evaluated for its catalytic activity under the same conditions as in Table I. It is found that the propane conversion rate is 93.2 percent and the carbon monoxide purification efficiency is percent.
  • the warm-up characteristic of a honeycomb-structure carrier which had been provided with a film of palladium by the method of Example 1, was tested to determine the time needed for 100 percent purification of CO.
  • the results were excellent, being minutes against 7 minutes for PTX, i.e., the American Engelhards platinum catalyzer.
  • Example 4 The catalyzer used in Example 4 was prepared to the same size as the American Engelhards PTX No. 4 and under the test conditions specified by the Federal Test Process 1975 LA No. 4 mode, its gas purification ability was measured using an 1,800 CC engine. The results are given in Table 3.
  • the deposited metal salt is post-treated with a reducing agent or by heating to produce the catalyzer effect; and depending on the conditions of this treatment, there is wide variation in the catalytic effect produced.
  • a noble metal directly provides the catalyst layer; therefore, if the moisture penetrating fine pores can be removed by appropriate means, it will directly make a stable catalyst than can effectively exhibit the catalytic action.
  • a carrier of unit structure like a honeycomb carrier is extremely useful as a catalyst for purifying automobile exhaust gas because its vessel is easy to manufacture, it suffers little pressure loss, it possesses good warm-up characteristics, and it is free from abrasion wear.
  • the carrier should be built of a strong material.
  • Commonly preferred 'y-alumina for grain carrier which has a surface area of more than 100 m /g and has a high water absorption is hard to use; poor water absorbers with less than 10 m /g surface area such as a-alumina, cordierite or spodumenmullite are preferred.
  • These materials are complex in structure and are not suitable for evenly distributing the catalyst component; besides, it is difficult to make them carry the catalyst component by the impregnation method.
  • platinum with less surface area but greater effect has been selected heretofore as the preferred catalyst component; and it has been attempted to impregnate as much platinum as possible through immersion for a long time or under reduced pressure.
  • platinum is present'even at a depth where it takes no part in the reaction, the total platinum content amounting to as much as 0.3-0.5 weight percent which is extremely economically unfavorable.
  • a coating with a noble metal other than platinum, say, palladium can give as high activity as one with platinum.
  • the present invention even when applied to a carrier coated appropriately with a metal such as copper, nickel, cobalt, or chromium, or when additionally coated with a thin film of a metal oxide of copper, nickel, cobalt or chromium, can be equally effective or even synergistically effective.
  • a noble metal coat applied by the present invention is so full of pores that, when later immersed in a highly penetrating liquid, say, in a chromic acid solution, it permits penetration of the liquid into its depth; thus, when roasted, it can produce a synergist effect of chromium and a noble metal.
  • a process for producing a catalyst which comprises seeding a carrier by immersing said carrier in a first dilute solution containing a salt of a metal, drying the wet carrier by heating to thereby allow a precipitation core to deposit on the carrier surface and then, immersing the thus obtained carrier in a second solution containing a salt of the noble metal, a reducing agent selected from the group consisting of formalin, sodium formate, sodium hypophosphite, hydrazine, hydrosulfite, hydroboric acid, sodium borohydride, hydroquinone and urea and a stabilizer selected from the group consisting of the disodium salt of ethylene diamine tetra acetic acid, Rochelle salt, sodium glycolate, sodium malate, sodium lactate, sodium tartrate, sodium citrate, ammonium chloride, ammonium nitrate, ammonium sulfate, methyl ethyl ketone, acetone and 2,2- dithio-ethanol, to thereby form a film of the
  • a process for producing a catalyst according to claim 1 wherein said metal salt for the first immersion step is selected from the group consisting of gold chloride, platinum chloride, rhodium chloride, palladium chloride, gold nitrate, platinum nitrate, rhodium nitrate, and palladium nitrate.
  • a process for producing a catalyst according to claim 1 wherein said noble metal salt for said second solution is selected from the group consisting of chloroplatinic acid, platinum chloride, palladium nitrate, palladium sulfate, tetraamine palladium, rhodium chloride, rhodium sulfate and rhodium nitrate.
  • concentration of said metal salt in said second solution for catalyzer film formation is 0.005 to 0.1 mole per liter.
  • a method for producing a catalyst according to 5 Solution is 0-001 to 005 mol P literclaim 1 wherein concentration of said reducing agent UNITED STATES PATENT ()FEICE CERTIFICATE OF CORRECTION Patent No. 3,816,344 Dated June 11, L974 It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:

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  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Biomedical Technology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Catalysts (AREA)
  • Chemically Coating (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
US00265449A 1971-11-22 1972-06-23 Process for producing a catalyst Expired - Lifetime US3816344A (en)

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Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3919121A (en) * 1973-04-05 1975-11-11 Colonial Metals Inc Method for precipitating platinum metal on a support
US3953369A (en) * 1973-04-06 1976-04-27 Nippon Shokubai Kagaku Kogyo Co., Ltd. Method for the production of a platinum catalyst used for purification of exhaust and waste gases
US4119645A (en) * 1973-04-11 1978-10-10 Rhone-Progil Method of preparing phthalic anhydride
US4222856A (en) * 1977-06-09 1980-09-16 Air Products And Chemicals, Inc. Method for promoting regeneration of a catalyst in a fluidized regenerator
US4568450A (en) * 1982-08-19 1986-02-04 Union Oil Company Of California Hydrocarbon conversion process
US4716143A (en) * 1986-06-06 1987-12-29 Uop Inc. Dehydrogenation catalyst composition
US4743353A (en) * 1982-08-19 1988-05-10 Union Oil Company Of California Oxidation process
US4743359A (en) * 1982-08-19 1988-05-10 Union Oil Company Of California Reforming and related processes
US4762960A (en) * 1987-02-25 1988-08-09 Uop Inc. Dehydrogenation catalyst composition and paraffin dehydrogenation
US4774221A (en) * 1985-10-26 1988-09-27 Bayer Aktiengesellschaft Supported hydrogenation catalysts
US4827072A (en) * 1986-06-06 1989-05-02 Uop Inc. Dehydrogenation catalyst composition and hydrocarbon dehydrogenation process
US4835131A (en) * 1986-08-29 1989-05-30 Shell Oil Company Catalyst and process for the preparation of the catalyst
US5488024A (en) * 1994-07-01 1996-01-30 Phillips Petroleum Company Selective acetylene hydrogenation
US5600692A (en) * 1993-10-29 1997-02-04 General Electric Company Method for improving tenacity and loading of palladium on palladium-doped metal surfaces
US6147027A (en) * 1997-09-24 2000-11-14 Toyota Jidosha Kabushiki Kaisha Alloy catalyst and process for producing the same
US20040192792A1 (en) * 2002-12-30 2004-09-30 Conocophillips Company Catalysts for the conversion of methane to synthesis gas
US20110065572A1 (en) * 2008-05-22 2011-03-17 Dow Global Technologies Inc. Method for preparing a heterogeneous, high-activity platinum-containing, supported hydrogenation catalyst
KR20190024959A (ko) * 2016-07-04 2019-03-08 우에무라 고교 가부시키가이샤 무전해 백금도금욕
EP3363928A4 (en) * 2015-10-15 2019-06-19 Kojima Chemicals Co. Ltd. AUTOCATALYTIC PLATE PLATING SOLUTION

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5033992A (enrdf_load_stackoverflow) * 1973-07-31 1975-04-02
JPS5084487A (enrdf_load_stackoverflow) * 1973-12-01 1975-07-08
JPS5724178B2 (enrdf_load_stackoverflow) * 1973-12-05 1982-05-22
JPS561932B2 (enrdf_load_stackoverflow) * 1974-10-31 1981-01-16
JPS54142189A (en) * 1978-04-27 1979-11-06 Toyota Motor Corp Preparation of catalyst
JP2808639B2 (ja) * 1989-03-15 1998-10-08 松下電器産業株式会社 セラミック電子部品の電極用導電性粒子
JPH05112369A (ja) * 1991-10-18 1993-05-07 Takasago Denki Sangyo Kk 液体飲料充填用瓶

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3919121A (en) * 1973-04-05 1975-11-11 Colonial Metals Inc Method for precipitating platinum metal on a support
US3953369A (en) * 1973-04-06 1976-04-27 Nippon Shokubai Kagaku Kogyo Co., Ltd. Method for the production of a platinum catalyst used for purification of exhaust and waste gases
US4119645A (en) * 1973-04-11 1978-10-10 Rhone-Progil Method of preparing phthalic anhydride
US4222856A (en) * 1977-06-09 1980-09-16 Air Products And Chemicals, Inc. Method for promoting regeneration of a catalyst in a fluidized regenerator
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JPS5412435B2 (enrdf_load_stackoverflow) 1979-05-23

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